US4055415A - Process for the removal of alloying impurities in a slag-covered copper refining bath - Google Patents
Process for the removal of alloying impurities in a slag-covered copper refining bath Download PDFInfo
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- US4055415A US4055415A US05/677,777 US67777776A US4055415A US 4055415 A US4055415 A US 4055415A US 67777776 A US67777776 A US 67777776A US 4055415 A US4055415 A US 4055415A
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- 239000010949 copper Substances 0.000 title claims abstract description 173
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 title claims abstract description 133
- 229910052802 copper Inorganic materials 0.000 title claims abstract description 129
- 238000007670 refining Methods 0.000 title claims abstract description 44
- 238000000034 method Methods 0.000 title claims abstract description 28
- 238000005275 alloying Methods 0.000 title abstract description 22
- 239000012535 impurity Substances 0.000 title description 9
- 239000000203 mixture Substances 0.000 claims abstract description 93
- 239000002893 slag Substances 0.000 claims abstract description 54
- 229910052796 boron Inorganic materials 0.000 claims abstract description 36
- 229910052744 lithium Inorganic materials 0.000 claims abstract description 17
- 239000011734 sodium Substances 0.000 claims abstract description 15
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 14
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 claims abstract description 13
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 12
- 229910052708 sodium Inorganic materials 0.000 claims abstract description 12
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 claims abstract description 10
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000011575 calcium Substances 0.000 claims abstract description 10
- 239000010703 silicon Substances 0.000 claims abstract description 10
- 239000010936 titanium Substances 0.000 claims abstract description 10
- 239000007858 starting material Substances 0.000 claims abstract description 9
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims abstract description 8
- 239000011777 magnesium Substances 0.000 claims abstract description 8
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 8
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims abstract description 7
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910052791 calcium Inorganic materials 0.000 claims abstract description 7
- 229910052700 potassium Inorganic materials 0.000 claims abstract description 7
- 229910052712 strontium Inorganic materials 0.000 claims abstract description 7
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 claims abstract description 7
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims abstract description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 6
- 229910052788 barium Inorganic materials 0.000 claims abstract description 6
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 claims abstract description 6
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 6
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims abstract description 5
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000011591 potassium Substances 0.000 claims abstract description 5
- 238000004519 manufacturing process Methods 0.000 claims abstract description 3
- 238000003723 Smelting Methods 0.000 claims description 10
- 230000001590 oxidative effect Effects 0.000 claims description 8
- 229910000881 Cu alloy Inorganic materials 0.000 claims description 2
- 238000000151 deposition Methods 0.000 claims 1
- 229910052787 antimony Inorganic materials 0.000 description 43
- 229910052718 tin Inorganic materials 0.000 description 42
- 229910052725 zinc Inorganic materials 0.000 description 39
- 229910052785 arsenic Inorganic materials 0.000 description 24
- 229910052742 iron Inorganic materials 0.000 description 23
- 229910052760 oxygen Inorganic materials 0.000 description 23
- 229910052745 lead Inorganic materials 0.000 description 22
- 229910045601 alloy Inorganic materials 0.000 description 19
- 239000000956 alloy Substances 0.000 description 19
- 229910052759 nickel Inorganic materials 0.000 description 19
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 12
- 239000002023 wood Substances 0.000 description 10
- 239000000654 additive Substances 0.000 description 9
- 239000002775 capsule Substances 0.000 description 9
- 230000000996 additive effect Effects 0.000 description 8
- 229910052793 cadmium Inorganic materials 0.000 description 8
- 229910018274 Cu2 O Inorganic materials 0.000 description 7
- 230000003647 oxidation Effects 0.000 description 7
- 238000007254 oxidation reaction Methods 0.000 description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 229910002804 graphite Inorganic materials 0.000 description 6
- 239000010439 graphite Substances 0.000 description 6
- 230000003252 repetitive effect Effects 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 229910021529 ammonia Inorganic materials 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- MQWCQFCZUNBTCM-UHFFFAOYSA-N 2-tert-butyl-6-(3-tert-butyl-2-hydroxy-5-methylphenyl)sulfanyl-4-methylphenol Chemical compound CC(C)(C)C1=CC(C)=CC(SC=2C(=C(C=C(C)C=2)C(C)(C)C)O)=C1O MQWCQFCZUNBTCM-UHFFFAOYSA-N 0.000 description 2
- 239000005997 Calcium carbide Substances 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- CLZWAWBPWVRRGI-UHFFFAOYSA-N tert-butyl 2-[2-[2-[2-[bis[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]amino]-5-bromophenoxy]ethoxy]-4-methyl-n-[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]anilino]acetate Chemical compound CC1=CC=C(N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)C(OCCOC=2C(=CC=C(Br)C=2)N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)=C1 CLZWAWBPWVRRGI-UHFFFAOYSA-N 0.000 description 2
- 101150013124 Plce1 gene Proteins 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/006—Pyrometallurgy working up of molten copper, e.g. refining
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/0028—Smelting or converting
- C22B15/005—Smelting or converting in a succession of furnaces
Definitions
- the invention relates to a process for the pyrometallurgical production of high-grade copper by smelting and oxidizing a charge of starting material, and subjecting the resultant treated charge to slagging and reducing steps to complete the refining.
- An additional factor limiting the efficiency of refining is the fact that, with existing techniques, the relatively high dispersion of the impure oxides collected on the surface of the bath during smelting and oxidation prevents the effective separation, from the bath, of a significant portion of such impurities, whereby the unseparated impurities adhere to the lining of the smelting and oxidizing furnace. Such adhered impurities become reconverted to metal during the reduction step, thereby increasing the impurities content of the refined copper.
- a charge of starting copper-based material into high-grade copper.
- a charge of a relatively inexpensive starting material such as blister copper or copper scrap, is initially subjected to smelting and oxidation steps in a conventional manner. After slagging the resultant bath to obtain pre-refined copper, an artificial slag layer is deposited on top of the pre-refined bath.
- Such artificial slag layer is formed from a mixture of (1) an oxide of at least a first element selected from the group consisting of silicon, phosphorous and boron, and (2) an oxide of at least one second element selected from the group consisting of titanium, aluminum, calcium, strontium, barium, magnesium, sodium, potassium and lithium.
- At least two refining alloying components selected individually from the first and second groups of elements, are fed to the bottom of the pre-refined copper bath.
- the bath is then mixed for at least 30 seconds and preferably from 3-6 minutes, after which the bath is allowed to stand for at least 15 minutes.
- the artificial slag layer is removed, and the reduction step accomplished in a conventional manner.
- FIGURE is a representation of a pyrometallurgical apparatus for carrying out the improved process of the invention.
- a charge of starting material illustratively in the form of copper scrap or blister copper having a significant degree of impurities (e.g., as high as 4-5%) is introduced into a conventional gas or oil-fired shaft furnace 1 for smelting.
- the charge is led, illustratively on a continuous basis, into a rotary oxidizing furnace 2 of conventional construction.
- the oxidation is accomplished with the aid of oxygen introduced into the furnace 2 via a pipe 3 from a suitable source.
- the charge is led into a first chamber 4a of a double-chamber furnace 4.
- the charge is initially slagged to define a pre-refined copper bath.
- such slagging step is followed by the formation, on the surface of the pre-refined copper bath, an artificial slag layer 6.
- the slag layer includes an oxide of silicon, phosphorous or boron, taken singly or in combination, and an oxide of titanium, aluminum, calcium, strontium, barium, magnesium, sodium, potassium or lithium, taken singly or in combination.
- the oxides of the separate groups of elements are separately led to the surface of the pre-refined copper bath. It has been found advantageous to adjust the quantity of the slag layer 6 relative to the underlying charge so that the components of the slag layer are present in a quantity corresponding to 0.4-5.5% by weight (preferably 1.5-2% by weight) relative to the weight of the underlying charge.
- the alloying components include at least one constituent from the first group of elements whose oxides define the slag layer 6, i.e. silicon, phosphorous or boron.
- the second alloying component consists of an element from the second group whose oxide forms the remainder of the slag layer 6.
- the alloying components formed from the first and second groups of elements are preferably separately flowed in succession to the bottom of the chamber 4a, with the component having the silicon, phosphorous or boron constituent fed first.
- the component having the silicon, phosphorous or boron constituent fed first.
- such successive alloying components are flowed in succession at predetermined intervals, e.g., 5-15 minutes.
- the quantity of the added alloying components should be adjusted to 4-52% by weight (e.g., 10-15%) relative to the weight of the charge.
- the bath is mixed in the chamber 4a for at least 30 seconds, and illustratively 3-6 minutes.
- a second slagging operation is then accomplished in which the slag layer 6 is removed in batches through an aperture 7; advantageously, such second slagging operation is preceded by a quiescent interval of at least 15 minutes following the mixing step.
- Such second slagging step is effective to remove the high-dispersion impurity component which, in previous processes, adhered to the chamber walls to be re-converted to metal during a subsequent reduction step and to thereby increase the impurity of the final product.
- the pre-refined charge is introduced into a second chamber 4b of the furnace 4 through an aperture 51, where a conventional reduction operation takes place to complete the refining of the charge.
- the refined copper is conveyed to a suitable casting mold (not shown) through a pouring gate 8.
- the refining alloying components may be alloyed with pure copper before introduction to the pre-refined bath to obtain an alloy having a composition of about 90% copper.
- the copper was oxidized by adding 10 kg of Cu 2 O. After slagging, 2 kg of a synthetic slag cover of the following composition were formed on the surface of the bath:
- the bath was mixed with a graphite bar for 1 minute, then maintained at 1230° C for 20 minutes. Thereafter, slagging and reduction with ammonia gas were accomplished. 103.4 kg of refined copper of the following composition were obtained:
- the copper was oxidized by adding 10 kg of Cu 2 O. After slagging, 2 kg of a synthetic slag cover of the following composition were fed to the surface of the bath:
- the bath was mixed with a graphite bar for one minute, then maintained at a temperature of 1250° C for 15 minutes. After slagging and reduction with ammonia gas, 103.2 kg of copper of the following composition were obtained:
- the copper was smelted and oxidized with air blast to reach a Cu 2 O-content of 7% by weight. After slagging, 200 kg of a synthetic slag cover of the following composition were introduced:
- the batch was smelted and oxidized with an air blast to reach 10% by weight of Cu 2 O content. After slagging, 10 kg of a synthetic slag cover of the following composition was fed in:
- the copper was reduced by adding 10 kg of Cu 2 O followed by slagging. Then, 1.5 kg of a synthetic slag cover of the following composition were fed in:
- the bath was mixed with a graphite bar for one-half minute, then kept at a temperature of 1210° C for 15 minutes.
- the copper was oxidized by adding 1.7 kg of Cu 2 O. After slagging, 0.5 kg of a synthetic slag cover of the following composition was fed in:
- the bath was mixed with a garphite bar for 30 seconds, then left to rest for 15 minutes. After slagging, the bath was reduced with ammonia gas. 104.6 kg of copper of the following composition were obtained:
- the copper was oxidized by adding 7 kg of Cu 2 O. After slagging, 0.5 kg of a synthetic slag cover of the following composition was added:
- the bath was mixed with a graphite bar for one-half minute, then left to rest for 15 minutes. After slagging and reduction with ammonia gas, 104.3 kg of copper of the following composition were obtained:
- the copper was oxidized by adding 10 kg of Cu 2 O. After slagging, 0.5 kg of a synthetic slag cover of the following composition were fed in:
- the lithium component was placed under vacuum into a copper capsule before feed-in.
- Converter copper of the following composition was smelted in a shaft furnace at the rate of 1 ton/hour:
- the smelted copper was flowed through a channel into a 1-ton revolving-type furnace, in which 5% by weight Cu 2 O-content was continuously attained via an air blast. From here, the copper was flowed at a continuous rate to a double-chamber furnace into the first chamber of which 10 kg of a synthetic slag cover of the following composition was fed in:
- the slag cover was removed after 1 hour. An additional 10 kg of synthetic slag cover of identical composition was then fed onto the top of the bath. A refining alloy, in 0.5 kg batches each of the following composition, was then fed at 15 -minute intervals to the bottom of the copper bath in the first chamber of the double-chamber furnace:
- the so-obtained copper was of the following composition:
- the smelted copper was flowed into the furnace according to Example 12, in which it was oxidized until reaching a Cu 2 O-content of 6% by weight. From here, the copper was flowed at a continuous rate to a double-chamber furnace, into the first chamber of which a synthetic slag cover of the following composition was fed at the rate of 50 kg/hour:
- the slag was removed every hour. Alloying components formed from the following materials were successively conducted to the bottom of the bath at repetitive 5-minute intervals: (1) 0.5 kg of silicon; (2) 0.5 kg of phosphorous; (3) 0.5 kg of boron; and (4) 0.5 kg of calcium carbide. A total of 6 kg of refining alloying components were conducted to the bath every hour. Reduction was carried out in the second chamber of the furnace with natural gas. The obtained copper was of the following composition:
- Copper blocks of the following composition were continuously smelted in a shaft furnace at the rate of 4 tons/hour:
- the smelted copper was flowed through a channel into a 12-ton revolving drum-type furnace, wherein 6% by weight of Cu 2 O-content was obtained by continuous oxidation with an air blast. From here, the copper was flowed at a continuous rate to a double-chamber furnace into the first chamber of which 70 kg of a synthetic slag cover of the following composition were fed in:
- the slag was changed every hour.
- the following elements, closed in a copper capsule, were successively fed to the bottom of the copper bath at repetitive 5-minute intervals in the first chamber of the double-chamber furnace: (1) 0.8 kg of silicon; (2) 1.1 kg of boron; (3) 0.5 kg of barium and strontium; (4) 0.4 kg titanium; (5) 1 kg of sodium; and (6) 0.2 kg of lithium.
- a total of 8 kg of refining alloying components were fed in per hour.
- the obtained copper was of the following composition:
- Copper blocks of the following composition were continuously smelted in a shaft furnace at the rate of 4 tons/hour:
- the smelted copper was flowed through a channel into a 12-ton revolving drum-type furnace, in which oxidation with an air blast at a continuous rate resulted in a Cu 2 O-content of 5% by weight. From here, the copper was flowed at a continuous rate to a double-chamber furnace, into the first chamber of which a synthetic slag cover of the following composition was fed at a rate of 60 kg/hour:
- the slag was changed every hour.
- the following elements in a copper capsule
- Such refining alloying components were fed into the bath at a rate of 4 kg/hour.
- reduction was carried out with cracked ammonia.
- the obtained copper was of the following composition:
- the copper was smelted by gas firing, oxidized by an air blast to reach 7% by weight of Cu 2 O-content, and then slagged. Thereafter 100 kg of synthetic slag cover of the following composition was fed in:
- the bath was mixed for 10 minutes and slagged. Then, a further 40 kg of slag cover of the following composition were fed to the bath:
- Copper blocks of the following composition were continuously smelted in a shaft furnace at the rate of 4 tons/hour:
- the smelted copper was flowed through a channel into a 12-ton revolving drum-type furnace, in which a Cu 2 O-content of 7% by weight was attained at a continuous rate by oxidizing with air. From here, the copper was flowed at a continuous rate to a double-chamber furnace, into the first chamber of which a synthetic slag cover of the following composition was fed at the rate of 70 kg/hour:
- the slag was changed every hour.
- the following refining elements were successively fed to the bottom of the bath at repetitive 10-minute intervals: (1) 1.5 kg of phosphorous; (2) 1.2 kg of aluminum; and (3) 1.3 kg of calcium, in the form of calcium carbide. A total amount of 8 kg of refining elements were fed in per hour. Reduction was carried out in the second chamber of the furnace with natural gas.
- the obtained copper was of the following composition:
- Copper blocks of the following composition were continuously smelted in a shaft furnace at a rate of 4 tons/hour:
- the smelted copper was flowed into a 12-ton revolving drum-type furnace, in which an oxygen-content of 0.7% by weight was continuously attained by oxidation with air. From here, the copper was flowed at a continuous rate to a double-chamber furnace, into the first chamber of which a synthetic slag cover of the following composition was fed at a rate of 70 kg/hour:
- the slag was changed every hour.
- the following elements were conducted successively to the bottom of the bath at repetitive 7.5 -minute intervals: (1) 0.5 kg of silicon; (2) 1.2 kg of sodium; (3) 1.1 kg of phosphorous; and (4) 0.5 kg of lithium.
- the lithium and sodium had been enclosed in separate copper capsules under vacuum.
- a total of 6.6 kg of refining elements were fed in every hour.
- the composition of the copper obtained after subsequent reduction was as follows:
- the bath was mixed for 10 minutes, followed by slagging. Then, 80 kg of a synthetic slag cover of the following composition were fed onto the bath:
- the bath was mixed for 10 minutes, followed by slagging. Then, 220 kg of a synthetic slag cover of the following composition were fed onto the bath:
- the bath was mixed for 10 minutes, followed by slagging. Then 230 kg of a synthetic slag cover of the following composition were fed to the bath:
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Abstract
A relatively simple and rapid process for the production of high-grade copper from an inexpensive starting material such as blister copper or copper scraps is described. The starting material is conventionally smelted and oxidized, after which the charge is subjected to a slagging operation to obtain a pre-refined copper bath. After the slagging step, an artificial slag cover is formed on the pre-refined copper bath using a mixture of (1) an oxide of at least one element selected from the group consisting of silicon, phosphorous and boron, and (2) an oxide of at least one element selected from the group consisting of titanium, aluminum, calcium, strontium, barium, magnesium, sodium, potassium and lithium. At least two of such elements are then fed to the bath through the slag cover as alloying components. After such resulting bath is mixed for at least 30 seconds and is left standing for an additional 15 minutes, the slag cover is removed. A conventional reduction step may then be accomplished to complete the refining process.
Description
The invention relates to a process for the pyrometallurgical production of high-grade copper by smelting and oxidizing a charge of starting material, and subjecting the resultant treated charge to slagging and reducing steps to complete the refining.
Existing copper refining processes of this type, particularly when carried out on a continuous basis, have exhibited several disadvantages. In particular, they have generally been relatively slow and expensive, since it has been found difficult to obtain sufficiently pure copper on an industrial scale without subjecting the charge to multiple or repeated steps (e.g., smelting) during the process. In addition, it has been found that for separation of the impurities which accumulate on the top of the copper bath during the smelting and oxidizing steps, costly metals and chemicals have been required.
Moreover, with such prior techniques it has been possible to obtain high-grade copper only when the starting material has been of relatively high quality, e.g., high-grade copper ore.
An additional factor limiting the efficiency of refining is the fact that, with existing techniques, the relatively high dispersion of the impure oxides collected on the surface of the bath during smelting and oxidation prevents the effective separation, from the bath, of a significant portion of such impurities, whereby the unseparated impurities adhere to the lining of the smelting and oxidizing furnace. Such adhered impurities become reconverted to metal during the reduction step, thereby increasing the impurities content of the refined copper.
All of such disadvantages are overcome by the improved process in accordance with the invention for the pyrometallurgical refining of a charge of starting copper-based material into high-grade copper. Illustratively, a charge of a relatively inexpensive starting material, such as blister copper or copper scrap, is initially subjected to smelting and oxidation steps in a conventional manner. After slagging the resultant bath to obtain pre-refined copper, an artificial slag layer is deposited on top of the pre-refined bath. Such artificial slag layer is formed from a mixture of (1) an oxide of at least a first element selected from the group consisting of silicon, phosphorous and boron, and (2) an oxide of at least one second element selected from the group consisting of titanium, aluminum, calcium, strontium, barium, magnesium, sodium, potassium and lithium.
With the artificial slag layer in place, at least two refining alloying components, selected individually from the first and second groups of elements, are fed to the bottom of the pre-refined copper bath. The bath is then mixed for at least 30 seconds and preferably from 3-6 minutes, after which the bath is allowed to stand for at least 15 minutes. Then, the artificial slag layer is removed, and the reduction step accomplished in a conventional manner.
With the improved process, high-quality copper of purity as high as 99.99% can be obtained with a single electrolysis notwithstanding the use of inexpensive starting materials and inexpensive additives that make up the synthetic slag and the alloying components. In addition, the process permits considerable shortening of the time necessary for oxidation and reduction, and can be accomplished on a fully industrial scale.
The invention is further set forth in the following description taken in conjunction with the appended drawing in which the single FIGURE is a representation of a pyrometallurgical apparatus for carrying out the improved process of the invention.
The various steps of the improved process can be instrumented in the arrangement of FIG. 1 in the following way: A charge of starting material, illustratively in the form of copper scrap or blister copper having a significant degree of impurities (e.g., as high as 4-5%) is introduced into a conventional gas or oil-fired shaft furnace 1 for smelting. From the smelting furnace 1, the charge is led, illustratively on a continuous basis, into a rotary oxidizing furnace 2 of conventional construction. The oxidation is accomplished with the aid of oxygen introduced into the furnace 2 via a pipe 3 from a suitable source.
From the oxidizing furnace 2, the charge is led into a first chamber 4a of a double-chamber furnace 4. In the chamber 4a, the charge is initially slagged to define a pre-refined copper bath.
In accordance with the invention, such slagging step is followed by the formation, on the surface of the pre-refined copper bath, an artificial slag layer 6. The slag layer includes an oxide of silicon, phosphorous or boron, taken singly or in combination, and an oxide of titanium, aluminum, calcium, strontium, barium, magnesium, sodium, potassium or lithium, taken singly or in combination. Preferably, the oxides of the separate groups of elements are separately led to the surface of the pre-refined copper bath. It has been found advantageous to adjust the quantity of the slag layer 6 relative to the underlying charge so that the components of the slag layer are present in a quantity corresponding to 0.4-5.5% by weight (preferably 1.5-2% by weight) relative to the weight of the underlying charge.
With the slag layer in plce, at least two refining alloying components are introduced to the bottom of the chamber 4a via a graphite conduit 5. The alloying components include at least one constituent from the first group of elements whose oxides define the slag layer 6, i.e. silicon, phosphorous or boron. The second alloying component consists of an element from the second group whose oxide forms the remainder of the slag layer 6.
The alloying components formed from the first and second groups of elements are preferably separately flowed in succession to the bottom of the chamber 4a, with the component having the silicon, phosphorous or boron constituent fed first. In the preferred case where the refining operation takes place on a continuous basis, such successive alloying components are flowed in succession at predetermined intervals, e.g., 5-15 minutes. Additionally, the quantity of the added alloying components should be adjusted to 4-52% by weight (e.g., 10-15%) relative to the weight of the charge.
After the addition of the alloying components, the bath is mixed in the chamber 4a for at least 30 seconds, and illustratively 3-6 minutes. A second slagging operation is then accomplished in which the slag layer 6 is removed in batches through an aperture 7; advantageously, such second slagging operation is preceded by a quiescent interval of at least 15 minutes following the mixing step. Such second slagging step is effective to remove the high-dispersion impurity component which, in previous processes, adhered to the chamber walls to be re-converted to metal during a subsequent reduction step and to thereby increase the impurity of the final product.
Following the second slagging step, the pre-refined charge is introduced into a second chamber 4b of the furnace 4 through an aperture 51, where a conventional reduction operation takes place to complete the refining of the charge.
Following such refining step, the refined copper is conveyed to a suitable casting mold (not shown) through a pouring gate 8.
If desired, the refining alloying components may be alloyed with pure copper before introduction to the pre-refined bath to obtain an alloy having a composition of about 90% copper.
Without in any way limiting the generality of the foregoing, the following examples are presented to illustrate representative parameters of the inventive steps.
13,220 kg. of copper scraps of the following composition were fed into a 15-ton revolving gas-fired drum-type furnace:
______________________________________ Cu 98.7 % Sb 0.05% Fe 0.4 % Zn 0.3 % Ni 0.01% Sn 0.05% Pb 0.05% rest 0.39% As 0.05%. ______________________________________
300 kg of copper scale with 40 kg oxygen content were added to the batch, which was then smelted, oxidized with air to a Cu2 O-content of 6% by weight, and slagged. Then 60 kg of synthetic slag cover of the following composition was fed in:
______________________________________
SiO.sub.2 35% P.sub.2 O.sub.5
25.4%
CaO 10% B.sub.2 O.sub.3
29.6%.
______________________________________
This was followed by feeding 8.3 kg of a refining alloy having the following composition:
______________________________________ Si 33.3% B 33.4% P 33.3%. ______________________________________
These refining alloying components were fed into the covered batch after alloying with 200 kg of copper. Mixing for 10 minutes was followed by slagging and reduction with wood. 12,850 kg of copper of the following composition were obtained:
______________________________________ Cu 99.86 % Sb 0.004% Fe 0.001% Zn 0.001% Ni 0.001% Sn 0.005% Pb 0.002% O 0.05 % As 0.002%. ______________________________________
100 kg of impure copper blocks of the following composition were fed into a laboratory-type gas-fired reverbatory furnace:
______________________________________ Cu 97.2 % Sb 0.55% Fe 0.5 % Zn 0.4 % Ni 0.05% Sn 0.4 % Pb 0.25% rest 0.5 % As 0.15%. ______________________________________
The copper was oxidized by adding 10 kg of Cu2 O. After slagging, 2 kg of a synthetic slag cover of the following composition were formed on the surface of the bath:
______________________________________
TiO.sub.2 13.0% SrO 5.0%
P.sub.2 O.sub.5
47.8% K.sub.2 O
2.5%
B.sub.2 O.sub.3
15.2% Li.sub.2 O
8.5%
MgO 8.0%.
______________________________________
0.5 kg of a refining additive of the following composition, closed in a copper capsule under vacuum, was fed to the bottom of the covered bath:
______________________________________ Ti 0.1 kg Mg 0.1 kg P 0.1 kg K 0.06 kg B 0.1 kg Li 0.04 kg. ______________________________________
The bath was mixed with a graphite bar for 1 minute, then maintained at 1230° C for 20 minutes. Thereafter, slagging and reduction with ammonia gas were accomplished. 103.4 kg of refined copper of the following composition were obtained:
______________________________________ Cu 99.91 % Sb 0.003% Fe 0.001% Zn 0.002% Ni 0.004% Sn 0.005% Pb 0.005% O 0.02 % As 0.005%. ______________________________________
100 kg of impure copper blocks of the following composition were fed into a laboratory-type gas-fired reverbatory furnace:
______________________________________ Cu 97.2% Sb 0.55% Fe 0.5% Zn 0.4% Ni 0.05% Sn 0.4% Pb 0.25% rest 0.5% As 0.15%. ______________________________________
The copper was oxidized by adding 10 kg of Cu2 O. After slagging, 2 kg of a synthetic slag cover of the following composition were fed to the surface of the bath:
______________________________________
SiO.sub.2 20% CaO 10%
P.sub.2 O.sub.5
15% K.sub.2 O
15%
MgO 20% LiO.sub.2
20%.
______________________________________
0.7 kg of a refining additive of the following composition, closed in a copper capsule, was conducted to the bottom of the bath:
______________________________________ Si 0.1 kg Ca 0.1 kg P 0.4 kg K 0.1 kg Mg 0.2 kg Li 0.1 kg. ______________________________________
The bath was mixed with a graphite bar for one minute, then maintained at a temperature of 1250° C for 15 minutes. After slagging and reduction with ammonia gas, 103.2 kg of copper of the following composition were obtained:
______________________________________ Cu 99.93% Sb 0.002% Fe trace Zn trace Ni 0.003% Sn 0.004% Pb 0.005% 0 0.02% As 0.002%. ______________________________________
13,450 kg of copper blocks of the following compositions were fed into a 15-ton revolving drum-type reverbatory furnace:
______________________________________ Cu 96.3 % Sb 0.05% Fe 0.5 % Zn 1.6 % Ni 0.2 % Sn 0.1 % Pb 0.2 % Cd 0.5 % As 0.05% rest 0.5%. ______________________________________
The copper was smelted and oxidized with air blast to reach a Cu2 O-content of 7% by weight. After slagging, 200 kg of a synthetic slag cover of the following composition were introduced:
______________________________________
B.sub.2 O.sub.3
15% TiO.sub.2
10%
SiO.sub.2 5% SrO 15%
P.sub.2 O.sub.5
20% MgO 10%
Al.sub.2 O.sub.3
10% Li.sub.2 O
15%.
______________________________________
Thereafter 100 kg of a refining alloy of the following composition were conducted to the bottom of the bath:
______________________________________ B 5.1% Ti 8.7% Si 25.2% Sr 5.5% P 12.3% Mg 22.5% Al 20.5% Li 0.2%. ______________________________________
Mixing for 6 minutes was followed by 15 minutes of quiescence, after which slagging and reduction with wood took place. 12,500 kg of copper of the following composition were obtained:
______________________________________ Cu 99.85 % Sb 0.002% Fe 0.003% Zn 0.001% Ni 0.02 % Sn 0.008% Pb 0.006% O 0.05 %. ______________________________________
950 kg of impure copper block of the following composition were fed into a 1-ton gas-fired tipping furnace:
______________________________________ Cu 98.0 % As 0.5% Fe 0.06% Sb 0.5% Ni 0.01% Sn 0.4% Pb 0.03% rest 0.5%. ______________________________________
The batch was smelted and oxidized with an air blast to reach 10% by weight of Cu2 O content. After slagging, 10 kg of a synthetic slag cover of the following composition was fed in:
______________________________________
SiO.sub.2 10% P.sub.2 O.sub.5
20%
CaO 50% B.sub.2 O.sub.3
20%.
______________________________________
Thereafter a refining alloy, packed in copper plate, of the following composition were introduced:
______________________________________ CaC.sub.2 3.1 kg P 0.53 kg Si 1.34 kg B 0.13 kg. ______________________________________
Mixing for 10 minutes was followed by slagging and reduction with wood. 910 kg of refined copper of the following composition were obtained:
______________________________________
Cu 99.93 % As 0.005%
Fe 0.001% Sb 0.01 %
Ni 0.003% Sn 0.01 %
Pb 0.001% O 0.04 %.
______________________________________
100 kg of impure copper blocks of the following composition were fed into a laboratory-type gas-fired reverbatory furnace:
______________________________________
Cu 97.2 % Sb 0.55%
Fe 0.5 % Zn 0.4 %
Ni 0.05% Sn 0.4 %
Pb 0.25% rest 0.5 %
As 0.15%.
______________________________________
The copper was reduced by adding 10 kg of Cu2 O followed by slagging. Then, 1.5 kg of a synthetic slag cover of the following composition were fed in:
______________________________________
TiO.sub.2
15.8% SiO.sub.2
25 %
BaO 20.2% Li.sub.2 O
7.5%
Na.sub.2 O
31.5%.
______________________________________
0.3 kg of a refining alloy of the following composition closed under vacuum in a copper capsule were then conducted to the bottom of the bath:
______________________________________
Ti 0.1 kg Na 0.15 kg
Ca 0.05 kg.
______________________________________
The bath was mixed with a graphite bar for one-half minute, then kept at a temperature of 1210° C for 15 minutes.
After slagging and reduction with ammonia gas, 103.5 kg of copper of the following composition were obtained:
______________________________________
Cu 99.85 % Sb 0.003%
Fe 0.002% Zn 0.001%
Ni 0.006% Sn 0.007%
Pb 0.005% O 0.03 %
As 0.004%.
______________________________________
100 kg of impure copper blocks of the following composition were fed into a laboratory-type gas-fired reverbatory furnace:
______________________________________
Cu 98.9 % Sb 0.05%
Fe 0.3 % Zn 0.3 %
Ni 0.02% Sn 0.05%
Pb 0.06% rest 0.3 %
As 0.02%.
______________________________________
The copper was oxidized by adding 1.7 kg of Cu2 O. After slagging, 0.5 kg of a synthetic slag cover of the following composition was fed in:
______________________________________
P.sub.2 O.sub.5
75% TiO.sub.2
25%.
______________________________________
0.15 kg of a refining additive of the following composition, closed in a copper capsule, were then conducted to the bottom of the bath:
______________________________________
P 60% Ti 40%.
______________________________________
The bath was mixed with a garphite bar for 30 seconds, then left to rest for 15 minutes. After slagging, the bath was reduced with ammonia gas. 104.6 kg of copper of the following composition were obtained:
______________________________________
Cu 99.87 % Zn 0.001%
Fe 0.001% Sn 0.002%
Ni 0.001% O 0.03 %
Pb 0.002%.
______________________________________
100 kg of impure copper blocks of the following composition were fed into a laboratory-type gas-fired reverbatory furnace:
______________________________________ Cu 98.9 % Sb 0.05% Fe 0.3 % Zn 0.3 % Ni 0.02% Sn 0.05% Pb 0.06% rest 0.3 % As 0.02%. ______________________________________
The copper was oxidized by adding 7 kg of Cu2 O. After slagging, 0.5 kg of a synthetic slag cover of the following composition was added:
______________________________________
SiO.sub.2
50% Na.sub.2 O
50%.
______________________________________
0.15 kg of a refining additive of the following composition, closed under vacuum in a copper capsule, was conducted to the bottom of the bath:
______________________________________
Si 55% Al 45%.
______________________________________
The bath was mixed with a graphite bar for one-half minute, then left to rest for 15 minutes. After slagging and reduction with ammonia gas, 104.3 kg of copper of the following composition were obtained:
______________________________________
Cu 99.86 % Sb 0.002%
Fe 0.001% Zn 0.001%
Ni 0.001% Sn 0.002%
Pb 0.002% O 0.04 %
As 0.001%.
______________________________________
100 kg of impure copper blocks of the following composition were fed into a laboratory-type gas-fired reverbatory furnace:
______________________________________
Cu 98.9 % Sb 0.05%
Fe 0.3 % Zn 0.3 %
Ni 0.02% Sn 0.05%
Pb 0.06% rest 0.3 %
As 0.02%.
______________________________________
The copper was oxidized by adding 10 kg of Cu2 O. After slagging, 0.5 kg of a synthetic slag cover of the following composition were fed in:
______________________________________
B.sub.2 O.sub.3
55% CaO 45%.
______________________________________
Thereafter, 0.5 kg of a refining additive of the following composition was conducted to the bottom of the bath:
______________________________________
B 40% CaO 45%.
______________________________________
Thereafter, the bath was mixed with a graphite bar for one-half minute, then left to rest for 15 minutes. After slagging, the bath was reduced with ammonia gas. 104.1 kg of copper of the following composition were obtained:
______________________________________
Cu 99.88 % Sb 0.001%
Fe 0.001% Zn trace
Ni 0.001% Sn trace
Pb 0.001% O 0.05 %
As 0.001%.
______________________________________
14,200 kg of impure copper blocks of the following composition were fed into a 15-ton revolving drum-type gas-fired reverbatory furnace:
______________________________________
Cu 97.5 % Sb 0.01%
Fe 0.5 % Zn 0.8 %
Ni 0.3 % Sn 0.1 %
Pb 0.05% Cd 0.1 %
As 0.01% rest 0.63%.
______________________________________
The copper was melted and oxidized to reach a Cu2 O-content of 6.5% by weight. After slagging, 150 kg of a synthetic slag cover of the following composition were fed in:
______________________________________
SiO.sub.2
30% B.sub.2 O.sub.3
20%
Na.sub.2 O
30% Al.sub.2 O.sub.3
20%.
______________________________________
Thereafter 150 kg of an AlSi-alloy of the following composition were conducted to the bottom of the bath:
______________________________________
Al 65% Si 35%.
______________________________________
Following mixing for 3 minutes, the bath was left to rest for 20 minutes, then slagged and reduced with wood. 13,300 kg refined copper of the following composition were obtained:
______________________________________
Cu 99.88 % Sb 0.002%
Fe 0.002% Zn 0.001%
Ni 0.01 % Cd 0.001%
Pb 0.005% Sn 0.002%
As 0.005%.
______________________________________
13,500 kg of copper blocks of the following composition were fed into a 15-ton revolving drum-type gas-fired furnace:
______________________________________
Cu 97.2% Sb 0.1%
Fe 0.4% Zn 1.3%
Ni 0.1% Sn 0.1%
Pb 0.1% Cd 0.4%
As 0.05% rest 0.25%.
______________________________________
The copper was smelted, then oxidized with an air blast to reach a Cu2 O-content of 6.8% by weight. After slagging, 160 kg of a synthetic slag cover of the following composition were fed in:
______________________________________
SiO.sub.2
50% Na.sub.2 O
50%.
______________________________________
After this, the following refining alloying components were fed to the bottom of the bath:
______________________________________
Si 20 kg CaC.sub.2
20 kg
Li 10 kg.
______________________________________
The lithium component was placed under vacuum into a copper capsule before feed-in.
By rotating the furnace, mixing was carried out for 5 minutes, followed by quiescence for 15 minutes. After slagging and reduction with wood, 12,700 kg of copper of the following composition were obtained:
______________________________________
Cu 99.97 % Sb 0.005%
Fe 0.001% Zn 0.001%
Ni 0.002% Sn 0.001%
Pb 0.005% O 0.02 %
As 0.001%.
______________________________________
Converter copper of the following composition was smelted in a shaft furnace at the rate of 1 ton/hour:
______________________________________
Cu 99.1 % Sb 0.1 %
Fe 0.05% Zn 0.05%
Ni 0.07% Sn 0.1 %
Pb 0.1 % rest 0.38%
As 0.05%.
______________________________________
The smelted copper was flowed through a channel into a 1-ton revolving-type furnace, in which 5% by weight Cu2 O-content was continuously attained via an air blast. From here, the copper was flowed at a continuous rate to a double-chamber furnace into the first chamber of which 10 kg of a synthetic slag cover of the following composition was fed in:
______________________________________
SiO.sub.2
45% P.sub.2 O.sub.5
25%
CaO 10% B.sub.2 O.sub.3
20%.
______________________________________
The slag cover was removed after 1 hour. An additional 10 kg of synthetic slag cover of identical composition was then fed onto the top of the bath. A refining alloy, in 0.5 kg batches each of the following composition, was then fed at 15 -minute intervals to the bottom of the copper bath in the first chamber of the double-chamber furnace:
______________________________________
Si 27.5% Al 30%
P 17.5% Ca 20%
B 5 %.
______________________________________
After mixing and slagging, reduction was carried out in the second chamber of the double-chamber furnace with cracked ammonia. The so-obtained copper was of the following composition:
______________________________________
Cu 99.88 % As 0.001%
Fe 0.01 % Sb 0.002%
Ni 0.005% Zn 0.002%
Pb 0.001% O 0.03 %.
______________________________________
Scrap copper of the following composition was continuously smelted in a shaft furnace at the rate of 4 tons/hour:
______________________________________
Cu 98.8 % Sb 0.15%
Fe 0.2 % Zn 0.3 %
Ni 0.01% Sn 0.05%
Pb 0.1 % rest 0.38%
As 0.01%.
______________________________________
The smelted copper was flowed into the furnace according to Example 12, in which it was oxidized until reaching a Cu2 O-content of 6% by weight. From here, the copper was flowed at a continuous rate to a double-chamber furnace, into the first chamber of which a synthetic slag cover of the following composition was fed at the rate of 50 kg/hour:
______________________________________
SiO.sub.2
45% P.sub.2 O.sub.5
25%
CaO 10% B.sub.2 O.sub.3
20%.
______________________________________
The slag was removed every hour. Alloying components formed from the following materials were successively conducted to the bottom of the bath at repetitive 5-minute intervals: (1) 0.5 kg of silicon; (2) 0.5 kg of phosphorous; (3) 0.5 kg of boron; and (4) 0.5 kg of calcium carbide. A total of 6 kg of refining alloying components were conducted to the bath every hour. Reduction was carried out in the second chamber of the furnace with natural gas. The obtained copper was of the following composition:
______________________________________
Cu 99.92 % Sb 0.002%
Fe 0.01 % Zn 0.001%
Si 0.02 % Sn 0.002%
Pb 0.01 % O 0.04 %
As 0.001%.
______________________________________
Copper blocks of the following composition were continuously smelted in a shaft furnace at the rate of 4 tons/hour:
______________________________________
Cu 98.1 % Sb 0.25%
Fe 0.4 % Zn 0.5 %
Ni 0.01% Sn 0.05%
Pb 0.2 % rest 0.39%
As 0.1 %.
______________________________________
The smelted copper was flowed through a channel into a 12-ton revolving drum-type furnace, wherein 6% by weight of Cu2 O-content was obtained by continuous oxidation with an air blast. From here, the copper was flowed at a continuous rate to a double-chamber furnace into the first chamber of which 70 kg of a synthetic slag cover of the following composition were fed in:
______________________________________
SiO.sub.2
25% TiO.sub.2
10%
B.sub.2 O.sub.2
20% Na.sub.2 O
15%
BaO 15% Li.sub.2 O
5%
SrO 10%.
______________________________________
The slag was changed every hour. The following elements, closed in a copper capsule, were successively fed to the bottom of the copper bath at repetitive 5-minute intervals in the first chamber of the double-chamber furnace: (1) 0.8 kg of silicon; (2) 1.1 kg of boron; (3) 0.5 kg of barium and strontium; (4) 0.4 kg titanium; (5) 1 kg of sodium; and (6) 0.2 kg of lithium. A total of 8 kg of refining alloying components were fed in per hour.
Reduction with cracked ammonia was carried out in the second chamber of the double-chamber furnace. The obtained copper was of the following composition:
______________________________________ Cu 99.92 % As 0.001% Fe 0.005% Sb 0.002% Ni 0.002% Zn 0.002% Pb 0.001% O 0.04 %. ______________________________________
Copper blocks of the following composition were continuously smelted in a shaft furnace at the rate of 4 tons/hour:
______________________________________ Cu 99.1 % Sb 0.05% Fe 0.2 % Zn 0.01% Ni 0.01% Sn 0.02% Pb 0.1 % rest 0.46% As 0.05%. ______________________________________
The smelted copper was flowed through a channel into a 12-ton revolving drum-type furnace, in which oxidation with an air blast at a continuous rate resulted in a Cu2 O-content of 5% by weight. From here, the copper was flowed at a continuous rate to a double-chamber furnace, into the first chamber of which a synthetic slag cover of the following composition was fed at a rate of 60 kg/hour:
______________________________________
B.sub.2 O.sub.3
55% Li.sub.2 O 45%.
______________________________________
The slag was changed every hour. In the first chamber of the double-chamber furnace, the following elements (in a copper capsule) were successively fed to the bottom of the copper bath at repetitive 15-minute intervals: (1) 1.2 kg of boron; and (2) 0.8 kg of lithium. Such refining alloying components were fed into the bath at a rate of 4 kg/hour. In the second chamber of the double-chamber furnace, reduction was carried out with cracked ammonia. The obtained copper was of the following composition:
______________________________________ Cu 99.95 % Sb 0.001% Fe trace Zn trace Ni 0.001% Sn trace Pb 0.001% O 0.02 % As 0.001%. ______________________________________
14,850 kg of copper scraps of the following composition were fed into a 15-ton revolving drum-type furnace:
______________________________________ Cu 95.2% Sb 0.2% Fe 0.6% Zn 0.5% Ni 0.3% Sn 0.6% Pb 0.8% Cd 0.1% As 0.3% rest 1.4%. ______________________________________
The copper was smelted by gas firing, oxidized by an air blast to reach 7% by weight of Cu2 O-content, and then slagged. Thereafter 100 kg of synthetic slag cover of the following composition was fed in:
______________________________________
SiO.sub.2 45.3% P.sub.2 O.sub.5
39%
CaO 6 % B.sub.2 O.sub.3
9.7%.
______________________________________
After this, 100 kg of refining alloying components of the following composition were conducted to the bottom of the bath:
______________________________________ Si 33.3% B 33.4% P 33.3%. ______________________________________
The bath was then mixed for 10 minutes, followed by slagging. Then, 50 kg of synthetic slag cover of the following composition were fed to the bath:
______________________________________
CaO 71.4% P.sub.2 O.sub.5
15.1%
SiO.sub.2 10.5% B.sub.2 O.sub.3
3 %.
______________________________________
After this, a further 48.5 kg of refining alloy of the following elements were fed to the bottom of the bath after being smelted with pure copper so that an alloy is obtained containing 90% of copper and 10% of the following refining alloying components:
______________________________________ Al 97.5% P 1 % Si 1 % B 0.5%. ______________________________________
The bath was then mixed for 10 minutes, followed by slagging and reduction with wood. 13,900 kg of copper of the following composition were obtained:
______________________________________ Cu 99.85 % Sb 0.002% Fe 0.005% Zn 0.002% Ni 0.03 % Sn 0.006% Pb 0.008% O 0.06 % As 0.006%. ______________________________________
12,380 kg of copper scraps of the following composition are fed into the furnace of Example 16:
______________________________________ Cu 97.6 % Sb 0.5% Fe 0.3 % Zn 0.5% Ni 0.05% Sn 0.4% Pb 0.15% rest 0.4% As 0.1 %. ______________________________________
1,500 kg of oxidized cement copper with 62 kg oxygen content were then added to the batch, and the charge was smelted and oxidized until a Cu2 O-content of 7% by weight was reached. After slagging, 70 kg of a synthetic slag cover of the following composition were fed in:
______________________________________
SiO.sub.2 28.5% P.sub.2 O.sub.5
31.5%
CaO 20 % B.sub.2 O.sub.3
20 %.
______________________________________
Thereafter, 300 kg of a copper alloy containing 30 kg of refining alloying components with the following composition were conducted to the bottom of the tank:
______________________________________ Si 66.8% B 6.6% P 26.6%. ______________________________________
The bath was mixed for 10 minutes and slagged. Then, a further 40 kg of slag cover of the following composition were fed to the bath:
______________________________________
Al.sub.2 O.sub.3
25% P.sub.2 O.sub.5
21%
CaO 25% B.sub.2 O.sub.3
14%
SiO.sub.2 15%.
______________________________________
After this, 36 kg of a refining alloy of the following composition were fed to the bottom of the bath:
______________________________________ Ca 5% P 30% Al 45% B 5% Si 15%. ______________________________________
The bath was mixed for 10 minutes, followed by slagging and reduction with wood. 13,500 kg of copper of the following composition were obtained:
______________________________________ Cu 99.88 % Sb 0.002% Fe 0.001% Zn 0.001% Ni 0.005% Sn 0.005% Pb 0.003% O 0.04 % As 0.005%. ______________________________________
Copper blocks of the following composition were continuously smelted in a shaft furnace at the rate of 4 tons/hour:
______________________________________ Cu 98.1 % Sb 0.25% Fe 0.4 % Zn 0.5 % Ni 0.01% Sn 0.05% Pb 0.2 % rest 0.39% As 0.1 %. ______________________________________
The smelted copper was flowed through a channel into a 12-ton revolving drum-type furnace, in which a Cu2 O-content of 7% by weight was attained at a continuous rate by oxidizing with air. From here, the copper was flowed at a continuous rate to a double-chamber furnace, into the first chamber of which a synthetic slag cover of the following composition was fed at the rate of 70 kg/hour:
______________________________________
B.sub.2 O.sub.3
25% BaO 10%
P.sub.2 O.sub.5
35% Na.sub.2 O 30%.
______________________________________
The slag was changed every hour. The following refining elements were successively fed to the bottom of the bath at repetitive 10-minute intervals: (1) 1.5 kg of phosphorous; (2) 1.2 kg of aluminum; and (3) 1.3 kg of calcium, in the form of calcium carbide. A total amount of 8 kg of refining elements were fed in per hour. Reduction was carried out in the second chamber of the furnace with natural gas. The obtained copper was of the following composition:
______________________________________ Cu 99.87 % Sb 0.002% Fe trace Zn trace Ni 0.001% Sn 0.001% Pb 0.001% O 0.04 % As 0.001%. ______________________________________
Copper blocks of the following composition were continuously smelted in a shaft furnace at a rate of 4 tons/hour:
______________________________________ Cu 98.5% Sb 0.2 % Fe 0.3% Zn 0.5 % Ni 0.1% Sn 0.01% Pb 0.1% rest 0.19% As 0.1%. ______________________________________
The smelted copper was flowed into a 12-ton revolving drum-type furnace, in which an oxygen-content of 0.7% by weight was continuously attained by oxidation with air. From here, the copper was flowed at a continuous rate to a double-chamber furnace, into the first chamber of which a synthetic slag cover of the following composition was fed at a rate of 70 kg/hour:
______________________________________
SiO.sub.2 25% P.sub.2 O.sub.5
35%
Li.sub.2 O 40%.
______________________________________
The slag was changed every hour. The following elements were conducted successively to the bottom of the bath at repetitive 7.5 -minute intervals: (1) 0.5 kg of silicon; (2) 1.2 kg of sodium; (3) 1.1 kg of phosphorous; and (4) 0.5 kg of lithium. The lithium and sodium had been enclosed in separate copper capsules under vacuum. A total of 6.6 kg of refining elements were fed in every hour. The composition of the copper obtained after subsequent reduction was as follows:
______________________________________ Cu 99.88 % Sb 0.002% Fe 0.002% Zn trace Ni 0.001% Sn 0.001% Pb 0.002% O 0.03 % As 0.001%. ______________________________________
14,500 kg of copper scraps of the following composition were fed into a 15-ton, gas-fired revolving drum-type furnace:
______________________________________ Cu 95.1% Sb 0.2% Fe 0.8% Zn 0.6% Ni 0.2% Sn 1.0% Pb 0.9% Cd 0.3% As 0.2% rest 0.7%. ______________________________________
The copper was smelted and then oxidized with an air blast until a Cu2 O-content of 7% by weight was reached. After slagging, 150 kg of a synthetic slag cover of the following composition were fed in:
______________________________________
SiO.sub.2 45.3% P.sub.2 O.sub.5
39.0%
CaO 6 % B.sub.2 O.sub.3
9.7%.
______________________________________
After this, 220 kg of a refining additive of the following composition were conducted to the bottom of the bath:
______________________________________
Si 33.3% B 33.4%
P 33.3%.
______________________________________
The bath was mixed for 10 minutes, followed by slagging. Then, 80 kg of a synthetic slag cover of the following composition were fed onto the bath:
______________________________________
CaO 71.4% P.sub.2 O.sub.5
15.1%
SiO.sub.2 10.5% B.sub.2 O.sub.3
3.0%.
______________________________________
Thereafter, a further 130 kg of a refining alloy which had previously been smelted with pure copper so that the copper content of the obtained alloy amounted to 90% and the following refining alloy content to 10%, were fed to the bottom of the bath:
______________________________________
Al 97.5% P 1.0%
Si 1.0% B 0.5%.
______________________________________
The bath was mixed for 10 minutes, followed by slagging and by reduction with wood. 13,885 kg of copper of the following composition were obtained:
______________________________________
Cu 99.86 % Sb 0.002%
Fe 0.005% Zn 0.002%
Ni 0.04 % Sn 0.006%
Pb 0.008% O 0.05 %
As 0.006%.
______________________________________
14,500 kg of copper scraps of the following composition are fed into a gas-fired 15-ton revolving drum-type furnace:
______________________________________
Cu 95.4% Sb 0.3%
Fe 0.7% Zn 0.8%
Ni 0.2% Sn 0.8%
Pb 0.8% Cd 0.1%
As 0.2% rest 0.7%.
______________________________________
The copper was smelted and then oxidized with an air blast until a Cu2 O-content of 7% by weight was reached. After slagging, 500 kg of a synthetic slag cover of the following composition were fed in:
______________________________________
SiO.sub.2
45.3% P.sub.2 O.sub.5
39.0%
CaO 6.0% B.sub.2 O.sub.3
9.7%.
______________________________________
Thereafter, 100 kg of a refined additive of the following composition were conducted to the bottom of the bath:
______________________________________
Si 33.3% B 33.4%
P 33.3%.
______________________________________
The bath was mixed for 10 minutes, followed by slagging. Then, 220 kg of a synthetic slag cover of the following composition were fed onto the bath:
______________________________________
CaO 71.4% P.sub.2 O.sub.5
15.1%
SiO.sub.2
10.5% B.sub.2 O.sub.3
3.0%.
______________________________________
After this, 56 kg of a refining alloy, which had previously been smelted with pure copper so that the copper content of the obtained alloy amounted to 90% and the following refining alloy content to 10%, were fed to the bottom of the bath:
______________________________________
Al 97.5% P 1.0%
Si 1.0 % B 0.5%.
______________________________________
The bath was then mixed for 10 minutes followed by slagging and by reduction with wood. 13,080 kg of copper of the following composition were obtained:
______________________________________
Cu 99.86 % Sb 0.002%
Fe 0.005% Zn 0.002%
Ni 0.03 % Sn 0.006%
Pb 0.007% O 0.06 %
As 0.005%.
______________________________________
15,000 kg of copper scraps of the following composition were fed into a 15-ton revolving drum-type gas-fired furnace:
______________________________________
Cu 94.8% Sb 0.3%
Fe 0.9% Zn 1.0%
______________________________________
______________________________________
Ni 0.3% Sn 1.0%
Pb 0.7% Cd 0.1%
As 0.2% rest 0.7%.
______________________________________
The copper was smelted and then oxidized with an air blast until a Cu2 O-content of 7% by weight was reached. After slagging, 520 kg of a synthetic slag cover of the following composition were fed in:
______________________________________
SiO.sub.2
45.3% P.sub.2 O.sub.5
39.0%
CaO 6.0% B.sub.2 O.sub.3
9.7%.
______________________________________
Thereafter, 250 kg of a refining additive of the following composition were conducted to the bottom of the bath:
______________________________________
Si 33.3% B 33.4%
P 33.3%.
______________________________________
The bath was mixed for 10 minutes, followed by slagging. Then 230 kg of a synthetic slag cover of the following composition were fed to the bath:
______________________________________
CaO 71.4% P.sub.2 O.sub.5
15.1%
SiO.sub.2
10.5% B.sub.2 O.sub.3
3.0%.
______________________________________
After this, a further 130 kg of a refining alloy, which had previously been smelted with pure copper so that the copper content of the obtained alloy amounted to 90% and the following refining alloy content to 10%, were fed to the bottom of the bath:
______________________________________
Al 97.5% P 1.0%
Si 1.0% B 0.5%.
______________________________________
The bath was mixed for 10 minutes, followed by slagging and by reduction with wood. 13,950 kg of copper of the following composition were obtained:
______________________________________ Cu 99.84 % Sb 0.002% Fe 0.004% Zn 0.001% Ni 0.03% Sn 0.006% Pb 0.007% O 0.05% As 0.006%. ______________________________________
In the foregoing, some illustrative examples of the claimed process have been described. Many variations and modifications will now occur to those skilled in the art. It is accordingly desired that the scope of the appended claims not be limited to the specific disclosure herein contained.
Claims (12)
1. In a process for the pyrometallurgical production of high-grade copper from a starting material selected from the group consisting of blister copper and copper scraps, the process comprising the successive steps of smelting and oxidizing a charge of the starting material, slagging the smelted and oxidized charge to obtain a pre-refined copper bath, and reducing the pre-refined copper bath to complete the refining, the improvement which comprises the further steps, accomplished between the slagging and reduction steps, of forming seconds the pre-refined copper bath an artificial slag cover consisting of a mixture of an oxide of at least one first element selected from the group consisting of silicon, phosphorous and boron and an oxide of at least one second element selected from the group consisting of titanium, aluminum, calcium, strontium, barium, magnesium, sodium, potassium and lithium, contacting the resulting covered bath with at least two elements selected from the group consisting of silicon, phosphorous, boron, titanium, aluminum, calcium, strontium, barium, magnesium, sodium, potassium and lithium, mixing the resulting bath for a first interval of at least 30 seconds, duration, maintaining the mixed bath in a rest condition for at least an additional 15 minutes, and then removing the artificial slag cover.
2. A process as defined in claim 1, in which the first interval of the mixing step is in the range of 3-6 minutes.
3. A process as defined in claim 1, in which the contacting step is accomplished by flowing the first and second elements in succession into the pre-refined copper bath.
4. A process as defined in claim 3, in which the smelting, oxidizing, slagging and reducing steps are accomplished on a continuous basis, and in which the step of flowing the first and second elements in succession into the pre-refined copper bath is repeated at regular second intervals.
5. A process as defined in claim 4, in which the second intervals are in the range of 5-15 minutes.
6. A process as defined in claim 1, in which the quantity of elements contacting the pre-refined copper bath amounts to 4-52% by weight relative to the amount of charge.
7. A process as defined in claim 6, in which the amount of elements amounts to 10-15% by weight relative to the amount of charge.
8. A process as defined in claim 7, in which the contacting step is accomplished by allowing the elements with copper, and then feeding the resulting copper alloy to the bath.
9. A process as defined in claim 1, in which the forming step is accomplished by separately depositing the oxides of the first and second elements on the top of the pre-refined copper bath.
10. A process as defined in claim 1, in which the quantity of slag cover formed on the top of the pre-refined copper bath amounts to 0.4-5.5% by weight relative to the weight of the charge.
11. A process as defined in claim 10, in which the quantity of the slag cover amounts to 1.5-2% by weight of the charge.
12. A process as defined in claim 1, in which the contacting step is accomplished by feeding the elements to the bottom of the bath.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| HUCE1040 | 1975-04-16 | ||
| HUCE1040A HU169980B (en) | 1975-04-16 | 1975-04-16 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4055415A true US4055415A (en) | 1977-10-25 |
Family
ID=10994216
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US05/677,777 Expired - Lifetime US4055415A (en) | 1975-04-16 | 1976-04-16 | Process for the removal of alloying impurities in a slag-covered copper refining bath |
Country Status (18)
| Country | Link |
|---|---|
| US (1) | US4055415A (en) |
| JP (1) | JPS51133125A (en) |
| AT (1) | AT357776B (en) |
| BE (1) | BE840780A (en) |
| CS (1) | CS203120B2 (en) |
| DD (1) | DD124259A5 (en) |
| DE (1) | DE2616653A1 (en) |
| FI (1) | FI65809C (en) |
| FR (1) | FR2307881A1 (en) |
| GB (1) | GB1507759A (en) |
| HU (1) | HU169980B (en) |
| IN (1) | IN143749B (en) |
| IT (1) | IT1059114B (en) |
| LU (1) | LU74754A1 (en) |
| NL (1) | NL7604034A (en) |
| RO (1) | RO75066A (en) |
| SE (1) | SE422596B (en) |
| YU (1) | YU39961B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4315775A (en) * | 1979-11-28 | 1982-02-16 | Southwire Company | Continuous melting and refining of secondary and/or blister copper |
| US4451289A (en) * | 1980-11-28 | 1984-05-29 | Metallurgie Hoboken-Overpelt | Process for extracting non-ferrous metals from iron-bearing scraps |
| US6395059B1 (en) | 2001-03-19 | 2002-05-28 | Noranda Inc. | Situ desulfurization scrubbing process for refining blister copper |
| US6478847B1 (en) | 2001-08-31 | 2002-11-12 | Mueller Industries, Inc. | Copper scrap processing system |
| EP2716776A4 (en) * | 2011-05-24 | 2015-03-11 | Jiangxi Rare Earth & Rare Met | Combined furnace system for fire refining red impure copper |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5481121A (en) * | 1977-12-13 | 1979-06-28 | Sumitomo Electric Ind Ltd | Process for refining electroconductive copper |
| JPS61231128A (en) * | 1985-04-03 | 1986-10-15 | Dowa Mining Co Ltd | Method for refining copper |
| HU209327B (en) * | 1990-07-26 | 1994-04-28 | Csepel Muevek Femmueve | Process for more intensive pirometallurgic refining primere copper materials and copper-wastes containing pb and sn in basic-lined furnace with utilizing impurity-oriented less-corrosive, morestaged iron-oxide-based slag |
| DE69229387T2 (en) * | 1991-07-15 | 2000-03-23 | Kabushiki Kaisha Kobe Seiko Sho, Kobe | METHOD FOR CLEANING COPPER RAW MATERIAL FOR COPPER OR ITS ALLOYS |
| JP2515071B2 (en) * | 1991-10-28 | 1996-07-10 | 株式会社神戸製鋼所 | Copper dissolution method |
| DE10231228B4 (en) * | 2002-07-11 | 2004-09-30 | Guido Koschany | Recovery of valuable materials from spark plugs and glow plugs |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1945074A (en) * | 1930-11-11 | 1934-01-30 | United Verde Copper Company | Recovery of selenium |
| DE1181921B (en) * | 1963-02-21 | 1964-11-19 | Ver Deutsche Metallwerke Ag | Process for treating melts made from alloys with a high copper content |
| US3262773A (en) * | 1962-02-22 | 1966-07-26 | Norddeutsche Affinerie | Process for the removal of arsenic, antimony, tin and other acid oxide producing impurities from copper |
| US3528803A (en) * | 1966-12-28 | 1970-09-15 | Hitachi Cable | Method for manufacturing oxygen-free copper by casting |
| US3561952A (en) * | 1968-02-05 | 1971-02-09 | William B Greenberg | Copper-refining method |
| US3682623A (en) * | 1970-10-14 | 1972-08-08 | Metallo Chimique Sa | Copper refining process |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE594650C (en) * | 1932-06-08 | 1934-03-20 | Electrochimie D Electrometallu | Process for the production of low-oxygen copper |
| BE401227A (en) * | 1933-03-13 | |||
| BE421815A (en) * | 1936-06-16 |
-
1975
- 1975-04-16 HU HUCE1040A patent/HU169980B/hu unknown
-
1976
- 1976-04-13 LU LU74754A patent/LU74754A1/xx unknown
- 1976-04-13 YU YU937/76A patent/YU39961B/en unknown
- 1976-04-13 GB GB14949/76A patent/GB1507759A/en not_active Expired
- 1976-04-13 FR FR7610777A patent/FR2307881A1/en active Granted
- 1976-04-14 SE SE7604406A patent/SE422596B/en not_active IP Right Cessation
- 1976-04-14 FI FI761015A patent/FI65809C/en not_active IP Right Cessation
- 1976-04-15 BE BE166185A patent/BE840780A/en not_active IP Right Cessation
- 1976-04-15 NL NL7604034A patent/NL7604034A/en not_active Application Discontinuation
- 1976-04-15 RO RO7685638A patent/RO75066A/en unknown
- 1976-04-15 CS CS762508A patent/CS203120B2/en unknown
- 1976-04-15 AT AT276276A patent/AT357776B/en active
- 1976-04-15 DE DE19762616653 patent/DE2616653A1/en active Granted
- 1976-04-15 DD DD192404A patent/DD124259A5/xx unknown
- 1976-04-15 IT IT22333/76A patent/IT1059114B/en active
- 1976-04-16 JP JP51043466A patent/JPS51133125A/en active Pending
- 1976-04-16 US US05/677,777 patent/US4055415A/en not_active Expired - Lifetime
- 1976-04-17 IN IN659/CAL/76A patent/IN143749B/en unknown
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1945074A (en) * | 1930-11-11 | 1934-01-30 | United Verde Copper Company | Recovery of selenium |
| US3262773A (en) * | 1962-02-22 | 1966-07-26 | Norddeutsche Affinerie | Process for the removal of arsenic, antimony, tin and other acid oxide producing impurities from copper |
| DE1181921B (en) * | 1963-02-21 | 1964-11-19 | Ver Deutsche Metallwerke Ag | Process for treating melts made from alloys with a high copper content |
| US3528803A (en) * | 1966-12-28 | 1970-09-15 | Hitachi Cable | Method for manufacturing oxygen-free copper by casting |
| US3561952A (en) * | 1968-02-05 | 1971-02-09 | William B Greenberg | Copper-refining method |
| US3682623A (en) * | 1970-10-14 | 1972-08-08 | Metallo Chimique Sa | Copper refining process |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4315775A (en) * | 1979-11-28 | 1982-02-16 | Southwire Company | Continuous melting and refining of secondary and/or blister copper |
| US4451289A (en) * | 1980-11-28 | 1984-05-29 | Metallurgie Hoboken-Overpelt | Process for extracting non-ferrous metals from iron-bearing scraps |
| US6395059B1 (en) | 2001-03-19 | 2002-05-28 | Noranda Inc. | Situ desulfurization scrubbing process for refining blister copper |
| US6478847B1 (en) | 2001-08-31 | 2002-11-12 | Mueller Industries, Inc. | Copper scrap processing system |
| US6579339B1 (en) | 2001-08-31 | 2003-06-17 | Mueller Industries, Inc. | Copper scrap processing system |
| EP2716776A4 (en) * | 2011-05-24 | 2015-03-11 | Jiangxi Rare Earth & Rare Met | Combined furnace system for fire refining red impure copper |
Also Published As
| Publication number | Publication date |
|---|---|
| CS203120B2 (en) | 1981-02-27 |
| DD124259A5 (en) | 1977-02-09 |
| IT1059114B (en) | 1982-05-31 |
| IN143749B (en) | 1978-01-28 |
| FI65809C (en) | 1984-07-10 |
| YU93776A (en) | 1982-06-30 |
| JPS51133125A (en) | 1976-11-18 |
| BE840780A (en) | 1976-08-02 |
| AT357776B (en) | 1980-07-25 |
| FR2307881B1 (en) | 1980-08-01 |
| GB1507759A (en) | 1978-04-19 |
| FI65809B (en) | 1984-03-30 |
| YU39961B (en) | 1985-06-30 |
| ATA276276A (en) | 1979-12-15 |
| DE2616653C2 (en) | 1987-07-23 |
| DE2616653A1 (en) | 1976-10-28 |
| SE7604406L (en) | 1976-10-17 |
| LU74754A1 (en) | 1976-11-11 |
| FR2307881A1 (en) | 1976-11-12 |
| FI761015A7 (en) | 1976-10-17 |
| SE422596B (en) | 1982-03-15 |
| HU169980B (en) | 1977-03-28 |
| RO75066A (en) | 1981-03-30 |
| NL7604034A (en) | 1976-10-19 |
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